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Membrane and Desalination Technologies - TCE Moodle Website

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256 L.K. Wang et al.<br />

Salty Cheese Whey<br />

NaCl 1,200 kg<br />

Whey Solids 1,200 kg<br />

Total 20,000 kg<br />

Desalted Whey<br />

NaCl 65 kg<br />

Whey Solids 1,032 kg<br />

Total 5,000 kg<br />

Permeate<br />

Cream<br />

Cream<br />

Separator<br />

Removal of salts from a food processing water stream can also be accomplished by using<br />

ED or ion exchange; however, the capital costs of both ED <strong>and</strong> ion exchange are higher than<br />

that of NF.<br />

5.4. Recovery of Potato Starch Effluent Using RO<br />

UF<br />

NaCl 1,135 kg<br />

Whey Solids 168 kg<br />

Total 25,000 kg<br />

Balance<br />

Tank<br />

Water for<br />

Ultrafiltration<br />

10,000 kg<br />

For Disposal<br />

Fig. 6.15. Removal of salts from cheese whey permeate by NF.<br />

Clean-in-place<br />

Tank<br />

The Avebe Foxhol plant in the Netherl<strong>and</strong>s produces starch from potatoes (34). As shown<br />

in Fig. 6.16, potato production involves washing <strong>and</strong> grinding potatoes to produce pulpy<br />

liquor containing potato water, starch, <strong>and</strong> fibers. The starch is then extracted, refined, <strong>and</strong><br />

dried as a product. The starch extraction effluent is treated by centrifugation for the separation<br />

of fibers. The residual effluent from the centrifuge contains protein, sugars, <strong>and</strong> minerals at<br />

about 4% TS previously too dilute to recover. The plant originally discharged its 180 m 3 /h of<br />

effluent into the North Sea <strong>and</strong> Holl<strong>and</strong>’s canals without treatment, causing serious water<br />

pollution.<br />

A continuous RO cleaner production system is now operated at Avebe utilizing openchannel<br />

tubular RO membranes for h<strong>and</strong>ling of high TSS in the centrifuge effluent. With the<br />

continuous RO system (34–36), the centrifuge effluent is divided into two streams: (a) the RO<br />

permeate amounting to about 90 m 3 of water; <strong>and</strong> (b) the RO retentate having 8% TS <strong>and</strong><br />

about 90 m 3 of water. The RO permeate is recycled to the grinding operation for reuse, while<br />

the RO retentate is treated by steam heat, coagulation, <strong>and</strong> mechanical separation, which is<br />

then dried as a high grade protein concentrate (protomyl PF) that can be used as animal feed<br />

for small animals, such as piglets, poultry, dogs, cats, minks, etc. The residual potato water<br />

from mechanical protein separation is evaporated, concentrated to about 60% TS, <strong>and</strong>

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